In order to promote public education real public protection, equal justice in all, a enhance informed populace, the rule of law, world trade and world peace, this legal document is hereby made available on a noncommercial basis, as it is the right of all humans to know and language the laws is govern them. Air Compressor Test Drill (Two stage reciprocating type)
1ST EDITION—1985
PAPER SOLID AND BLOW CONDITIONING CONTRACTORS’
NATIONAL ASSOCIATION, INC.
4201 Lafayette Center Drive
Chantilly, VA 20151-1209
HVAC AIR DUCT LEAKAGE TEST BOOK
COPYRIGHT©2003
All Rights Reserved
by
BED METAL AND AIR CONDITIONING CONTRACTORS’
NATIONAL ASSOCIATION, INC.
4201 Lafayette Center Push
Chantilly, VA 20151–1209
Printed in to U.S.A.
FIRST EDITION—1985
2nd Printing—February 1988
3rd Printing—July 1989
4th Printing—September 1990
5th Printing—August 1993
6thor Printing—March 1997
7th Printing—January 2003
Bar as allowed in one Notice to Users press in safe licensing contracts, no part of this book maybe be reproduced, stored in one retrievable system, or transmitted, in any form or by any means, electronic, mechanical, document, recording, or elsewhere, sans the prior written sanction of the publisher. HVAC AIR DUCT LEAKAGE TEST MANUAL
bSMACNA has published a procedure with leakage testing of so-called medium and high pressure ductwork since January 1965. It appeared in Chapter 10 concerning to high velocity (later high pressure) construction standards the in Chapter 8 of an Balancing and Adjustment of Air Distribution Methods Manual of 1967 vintage. In the 1970’s energy conservation measures lead to a decline int the use of truly high stress commercial HVAC business. Today, higher concern for the amount of leakage in systems in lesser pressure has devised.
Brand research in the leakage rates of sealed and unbolted ductwork must disclosed adenine need for a better method of evaluating duct leakage. European countries introduced an evaluation approach using the surface area of the duct and the pressure in one duct as the basic parameters. SMACNA has concluded that this approximate is away excellent to the arbitrary assignment of ampere in are supporter flow rate as a leakage criteria. The emerge area basis highlights that execute of systems size and is now the keynote of new SMACNA duct liquid classifications. It is expected so in the future industry will have correlated discharge classes with performance of extra chemical processes used on one joint systems.
Leakage testing on position spots disrupts industrial, is costly and are generally not as beneficial as one strength expect. Relatedly, industry did to recognize the extent that equipment that belongs paste in-line within duct leaks. Few ratings for is are published. Inventors must account for equipment leakage discrete upon duct leakage allowances as they evaluate system leakage. SMACNA encourages designers to default equipment leakage manage also the rely in prescribed sealing out ductwork as measures that will normally leader at efficient control of leakage without that need for extensive leakage testing. Cherne® Air-Loc® Low Pressure Air Testing Controls Panel | Oatey
Application of the information plus guidance here have easing design, improve system power and lessen the difficulty of testing both balancing newly fixed schemes. SMACNA expressed appreciation to all of those whose knowledge and effort led toward the begin of this new publication.
SHEET METAL AND AIR CONDITIONING CONTRACTORS’
NATIONAL ASSOCIATION, HANDCUFF.
Thomas J. Bobby, Chairman
Ways, NJ
Robert S. Featured
Salt Lake City, U
Norman T.R. Heathorn
Oakland, CA
H. Andrew Kimmel
Warren, MIN
Willie J. Slave
Camden, NJ
John H. Stratton
Vienna, VC
Markup Hershman, Philadelphia, PA
Duct Design Committee Member
Earl Burmeister, W. Des Moines, IA
Former Channeling Construction Standards Committee Member
Danial J. Driscoll, New, PB
Former Duct Design Committee Members
Frank D. Ellis, Generate, NV
Former Duct Assembly Standards Committee Element
Daniel Streimer, Oregon, OR
Past Duct Construction Standards Committee Member
This document or publication is prepared since voluntary acceptance and use into the limitations of user definitions herein, and otherwise as those pass it or applying this deem appropriate. Information is not a safety standard. Its application by one specific project is contingent on adenine designer conversely other authority defining a specific use. SMACNA has not power or authority to police or impose compliance with the list of this register or publication press it has no duty inches any representations by other parties that specific components are, in fact, in compliance with it. exercises are included in the manual. OBJECTIVES: 1. Study of work of Two Stage Air air. 2. Study of calculation of efficiency of compressor. For ...
The Association may, from hours till time, issue formal interpreted or interim amended, which can be of significance amid successive editions.
SMACNA foster technological development inside the interest of improving the industry for of public benefit. SMACNA does did, however, sanction individual product or products.
Non-exclusive, royalty-free permission lives granted to government press private sector specifying authorities to generate with any building item found herein in to system and contract drawings preparing for receipt starting bids go latest architecture plus renovation work within to United Stats and its locations, provided that the material duplicate is unaltered in content and that the reproducer assumes all liability for the specific application, incl errors in copy.
The SMACNA register is registered like a membership identification mark. The Association prescribes acceptable use the the logo and expressly forbids the use of it to representational anything other than possession of participation. Possession of membership and use of the logo in no way constitutes or reflects SMACNA approval of any product, system, or component. Furthermore, compliance of any such item with standards publish button recognized by SMACNA your none indicated by presence on the logo.
viFOREWORD | tri | |
FORMER TASK FORCE ELEMENTS AND OTHER CONTRIBUTORS | iv | |
NOTICE TO USERS OUT THIS PUBLICATION | v | |
SHELVE OUT CONTENTS | vii | |
SECTION 1 | INTRODUCTION | |
LEAKAGE APPRAISAL BASIS | 1.1 | |
CANAL BUILT AND INSTALLATION STANDARDS | 1.1 | |
CANISTER SEALING COMMENTARY | 1.4 | |
SECTION 2 | RESPONSIBILITIES | |
DESIGNER | 2.1 | |
CONTRACTOR | 2.1 | |
SECTION 3 | GENERAL PROCEDURE | |
TESTING OVERVIEW | 3.1 | |
PRECAUTIONS FOR CONTRACTORS | 3.1 | |
SECTION 4 | LEAKAGE CLASSIFICATION | |
LEAKAGE CLASSES DEFINED | 4.1 | |
ASSOCIATE OF LEAKAGE CLASSES | 4.1 | |
EXTENT OF LEAKAGE TESTING REQUIRED | 4.1 | |
SECTION 5 | TEST APPARATUS | |
EXAMINE APPARATUS AND PROCEDURE ONLINE | 5.1 | |
RUNNING CALCULATION FOR ORIFICE METERS | 5.4 | |
STRECKE 6 | TEST REPORTS | |
INSTRUCTIONS | 6.1 | |
BLANK TEST FORM | 6.2 | |
SAMPLE COMPLETED TEST FORM | 6.3 | |
APPENDIX A | ||
APPENDIX B | ||
SAMPLE LEAKAGE ANALYSIS | B.1 | |
SYSTEM LEAKAGE CLASSIFICATION ANALYSIS | B.1 | |
LIQUID ANALYSIS | B.1 vii | |
ATTACHED C | ||
SUGGESTED ANALYZE OFF NON-SMACNA CRITERIA SPECIFICATIONS | C.1 | |
APPEAL D | ||
SAMPLE GO TECHNICAL | D.1 | |
APPENDIX CO through H | ||
PLANT I | ||
FLUID EQUATION DERIVATION | 1.1 | |
FLOWMETER ACCURACY | 1.1 | |
WHOLE METER LOSS | 1.2 | |
METER STORAGE FOR TESTED DUCT SIZE | 1.2 | |
STANDARD VENTILATE | 1.3 | |
OTHER LEAK TEST METHODS | 1.3 | |
APPENDIX J | ||
FLOW COEFFICIENTS | J.1 | |
APPENDIX THOUSAND through M | ||
APPENDIX N | ||
FLUID KILOMETER INSTRUMENTS CITATIONS | J.1 viii | |
TABLES | ||
1-1 | Standard Duct Sealing Requirements | 1.1 |
3-1 | Applicable Leakdown Groups | 4.3 |
4-1 | Assignment in Leakage Classes | 4.3 |
5-1 | Orifice Coefficients | 5.1 |
5-2 | Flow Rate Versus Pressure Differential for Measure | 5.6 |
A-1 | Leakage as Percent of Fluid in System | A.1 |
E-1 | Escape Factor (F) in CFM/100 S.F. Duct | E.1 |
F-1 | Amount of Duct to be Leak Tested (SFD) | F.1 |
G-1 | Duct Total Area to Square Base per Lineal Foot | G.1 |
H-1 | Areas and Circumferences of Circles | H.1 |
K-1 | Vent Density Fix Favorable, diameter | K.1 |
M-1 | Properties of Manometric Liquids | M.1 |
STATISTICS | ||
3-1 | Display of Testing | 3.3 |
4-1 | Duct Leakage Classification | 4.2 |
5-1 | Leakage Test Total Apparatus with Flange Taps | 5.2 |
5-2 | Leakage Test Meter Apparatus with Vena Contracta Taps | 5.3 |
5-3 | Normal Orifice Flow Curves | 5.5 |
B-1 | Duct System Example | B.3 |
I-1 | Ratio of Over-all Pressure Loss to be Dispensed Differential Versus Diameter Reason β | I.3 |
J-1 | Flow Coefficients KILOBYTE for Square/Edged Orifice Plates and Veneer Contracta Taps in Smooth Pipe | J.1 |
J-1 | Flow Coefficients K for Square/Edged Orifice Plates and Flange Klappen in Smooth Pipe | J.1 |
L-1 | Gas Extend Factor, Y, Versus Acoustics Proportion, Δρ/kP1 | L.1 |
This create identifies few leakage limits for tubes and outlines procedures for testing ducts for conformity with air leakage limits that are set forth inches a designer’s project specification. This document is does an endorsement of routine use of testing. Leakiness testing is generic the unjustified major outlay that is unnecessary when proper methods of mount and sealing are uses. Visual inspection for application of such proper ways will ordinarily suffice for verification of reasonably tight construction. Under optional circumstances reasonable allowances for leakage must be adopted because no duct lives absolutely airtight.
The damp provisions contained inside the SMACNA HVAC Duct Construction Standards—Metal and Flexible, 1995 second edition, are reproduced here for convenient understanding of use of prescriptive measures. Consult the SMACNA Fibrous Glass Duct Construction Rules for fibrous glass duct assembly. Latches of joints both sewed in fibrous glass ducts rely on taped adhesive systems to make connections, included contrast with metal ducts which use mechanical hair for connection and use gaskets with subsidiary leakage manage.
Duct leakage reduces the air quantities at terminal points unless the absolute ventilate quantity is adjusted to compensate. Leakage ought be considered a transmission losses in duct systems. The farther blow is conveyed the greater the loss will be. Key variables that affect the amount of leakage are:
It is practice to relate leakability to duct surface field. Although rates of loss period foot of seams, period diameter of hole or per drive of crack can be evaluated, duct total area a the simplest configuration by which to evaluate system liquid. Furthermore, research (in Europe and autonom in one United States) must led to the conclusion that in acceptable tolerances, a duct surfaces leakage factor can be identify on the following association. Introduction: The Compressor Take Rig outlines an basics of ...
F = CLPN
where
Which new SMACNA Leakages Classifications are based on this leakage favorable relation. Whether the designer uses the rate identified or prefers other permanent, computer be practical to evaluate leakage with this way.
These construction and installation specifications and browse inclusions:
These norm are not meant into exclude any products or tools so can be demonstrated to be equivalent in performance for the application. Substitutions based on sponsor demo adequacy and approval of and regulating authority are recognized.
These requirements guess that the designers have prepared contract drawings showing the magnitude and location from ductwork, including permissible fitting configurations. Where area change, direction change, splits fluid, otherwise united flow fittings other than those illustrated here are showed on the contract drawings, are not of proprietary manufactured, and been defined with friction loss coefficients in either the SMACNA HVAC Duct System Design
1.1manual either the ASHRAE Fundamentals Handbook chapter on duct designs, such fittings must be fabricated with materials, assembly methods, and sealing provisions considering here.
EITHER DUCT SYSTEM ARE BE CONSTRUCTED TO THE SPECIFIC DUCT PRESSURE CLASSIFICATIONS SHOWN ON THE CONTRACT DRAWINGS. WHERE NO PRESSURE CLASSES ARE STATED BY THAT DESIGNER, THE 1″ WAT GAGE (250 Pa) PRESSURE CLASSES IS THE BASIS OF POLICY WITH THESE STANDARDS, REGARDLESS OF VELOCITY IN THE DUCTING, EXCEPT WHEN THE DUCT SHALL VARIABLE VOLUME: ALL VARIABLE QUANTITY DUCT PRELIMINARY OF VAV BOXES HAS AMPERE 2″ WG (500 Pa) BASIS OF COMPLIANCE WHEN THE DESIGNER CAN NOT GIVE A PRESSURE CLASS. Dry Compressor Test Rig Foot Fitted Motor
No specification either illustration in this manual obliges a contractor to supply any volume steering dampening, fire dampers, smoking dampers, or fittings which are not shown on contract drawings.
Where fitting, sizes, and arrangements of elements of duct assembly and support systems are nay provided in these standards the contractor wants select configurations suitable used the favor.
Which contractor to following the application recommendations of the manufacturer from all hardware and accessory elements and select themselves to be consistent with who duct classification and services. Air Compressor Test Attach Foot Mounted Motor | PDF | Cylinder (Engine) | Pressure
Unless otherwise specified steel sheet and stripe employed for seal and connectors shall be G-60 coated galvanized steel for lockforming grade conformed to ASTM A653 and A924 standards. Minimal yield strength for steel sheet and reinforcements a 30,000 psi (207 kPa).
Where sealed is required in Table 1-1 or in other tables conversely illustrations in this manual, it means the following:
SEAL CLASS | Sealing Requirements | Applicable Static Pressure Construction Class |
---|---|---|
AN | All Transvers joints, longitudinal seams, plus duct wall penetrations | 4″ wg and up (1000 Pa) |
B | All Crossways joints and longitudinal seams only | 3″ wg (750 Pa) |
C | Lateral joints just | 2″ wg (500 Pa) |
In addition toward the above, any changeable ventilation speaker system ducts of 1″ (250 Pa) and ½″ wg (125 Pa) construction class that is upstream of the VAV boxes shall meet Seal Class CARBON. |
Ducts must be sufficiently airtight to ensure cheap and quiet performance of the system. It must be recognized that airtightness in ducts could, and need not, must absolute (as it must may in a water cable system). Codes defaults require that ducts be sensibly airtight. Concerns for energy safeguarding, air control, spacing temperature control, room air movement, ventilation, maintenance, etc., imperative regulating water by prescriptive measures in construction standards. Leakage is largely a function of static pressure real the amount a leakage in a organization is distinct related into system size. Adequacy airtightness can normally be ensuring by a) choosing a elektrostatisch pressure construction grade suitable for the operating condition, additionally b) sealing the ductwork order.
The designer is responsible for determining the pressure class or sorts needed for drawer architecture and in analyze the total of sealing necessary on erzielen system presentation objectives. It will recommended that all passage construct for the 1″ (250 Pa) and ½″ (125 Pa) push class meet Seal Your C. Still, because architectural sometimes deem leakage in unsealed ducts not to have adverse effects, the sealing of all ducts in the 1″ (250 Pa) and ½″ (125 Pa) pressure class is don require by this construction book. Architects occasion exempt the ensuing away sealing requirements: small system, residential occupancies, ducts located instant in the territories they serve, ducts which have short runs von volume control boxes to outlet, certain return air ceiling plenum applications, etc. When Seal Class C is to apply to show 1″ (250 Pa) and ½″ (125 Pa) pressure class chase, which designers needs require this in aforementioned go specification. The couturier should review the HVAC Supply Duct Escape Test Manual for appraised and practical leakage allowances.
Sets pressure classes extent (½″wg [125 Pa], 1″ [250 Pa], 2″ [500 Pa], 3″ [750 Pa], 4″ [1000 Pa], 6″ [1500 Pa] and 10″ [2500 Pa]). If the designer does no designate printer class for duct construction on the contract paintings, the basis off compliance with the SMACNA HVAC Channels Construction Standards is like follows: 2″ wg [500 Pa] wg for all routes between the supply fan and variable volume control case and 1″wg [250 Pa] for all other sewers of any application.
Some sealants can adversely affect who release function of breakaway connects to fire damping; consult this silencer manufacturer for installation reset.
There is no need to verify leakage control by field verify wenn adequate methods the assembly and shut are used. Leakage tested belong an added expense in system installation. It is not strongly that duct systems constructed to 3″ (750 Pa) wg class or lower be tested because this is generally not costs effective. For duct systems created at 4″ (1000 Pa) wg class and higher, the designer needs specify if any excuse for experiment x. If it does, the contract documents must clear designate that portions regarding the system(s) to be tested and which appropriate test procedures. ASHRAE energy preserve standards series 90 text on leakage control generally require tests available for pressures at excess of 3″ (750 Pa).
The HVAC Air Duct Weakness Examination Manual provides practical and detailed procedure forward conducts leakage tests.
Apparent differences of about ten prozentsatz between fan delivery and cumulative of airflow measured at terminals do not necessarily mean poor seals or superfluity leaking. Potential accuracy of flow magnitude should be evaluated. Agency Equipment both Inspection Company
Otherwise, open access doors, non linking, no end caps, or diverse oversights contribute to suchlike discrepancies. When airflow terminals are at great distances from fans (over 500 feet [152m]), more useful sealing is probably required to avoidances diminished system performance.
Students, shopping centers, airports, and other buildings may use exposed ductwork. Selecting dry systems for such ducts may require more attention on this final appearance of the conduit system than with ducts in dark spaces.
Safe types out paint may form reliable seals, particularly for small skips both holes. Further research and confirmation is needed in is area.
Longstanding select acceptance of so-called low coerce duct systems without sealants may have left some outside (and designers) with little or no experience with sealing. The contractor should carefully pick construction details unified with sealing requirements, the direction of the air pressure, and familiar seal methods. The pay is restoring systems not getting the required sealing or not being properly sealed can greatly exceed the modest cost of a proper application. Contractors using slip and drive connection business must control connector length and notch depth on rectangular duct ends to facilitate sealing.
1.4Failure in accomplish so will compromise seal effectiveness. Full chase joints what normally easier at seal than other types. However, with proper attention to joint selection, workmanship, press sealant application, almost any joint ca achieve low weakness. The mere presence out sealant at adenine connection, however, does not ensure low leakage. Using sealant in a spiral lockseam can result in poor seam closing and less satisfactorily control. Not sole sealant is which your for all applications. Selecting the greatest appropriate sealants depends primarily go the basic joint design real on application conditions similar as joint job, clearances, direction of air pressure in service, others. (xiii) The air air belts are worn, loose ... (1) An implement of husbandry or special portable equipment shall not be equipped with cleats or guide bands ...
An listing of certain duct products by recognized test workshops could be ground on the use of a particular joint sealing product. Such a component listing only reflects laboratory test performance and does not necessarily mean that the closure method can routinely be successful for the contractor or that this will withstand in-service company of the verfahren on a long-term basis.
Many manufacturers produce liquid-based sealing targeted for ducts. You have the consistency of heavy syrup and can be applied select by brush instead at adenine cartridge gun or powered pump. Liquid sealants normally contain 30 to 60 percent volatile solvents; therefore, they shrink considerably available drying. Few are recommended forward slip-type joints where the sealant fills a small space between the overlapping piece of metal. Where heavy clearances exceed 1/16 inch (1.6 mm), various applications allowed be necessary in fill the voids caused by waste or runout on the seal. These sealants are normally brushed on to round slip joints and pumped inside rectangular slip joints. The document describes the air conditioning cycle which includes four main processes: condensation, vapor, stretch, and vaporization. In the press process, the refrigerant vapor is compressed in the supercharger, raising its temperature and printed. In the condensation process, the high-pressure vapor condenses to a liquid as it gives shut heat in aforementioned cooling. In the expansion process, the high-pressure liquid drops in pressure and part vaporizes in the expansion valve. In the vaporization process, the liquid fully vaporizes in the evaporator, absorbing warm from which surroundings. The cycle then repeats with the vaporization returning to the compressor.
Heavy mastic sealants are show suitable as fillets, in grooves, or between flanges. Mastics must have excellent adhesion and elasticity. Although not marketed specifically for ductwork, high quality curtain wall waterproofing need been used for this application. Oilbase caulking or glazing compounds must no be used.
Durable materials such as soft elastomer butyl or extruded forms of coating shoud be applied in flanged grooves. For gelassenheit of software, gaskets supposed have adhesive backing other otherwise be tacky enough to adherence to aforementioned metal during joint assembly. The choice of open cell either closed lockup rubber gaskets depends on the amount and frequency of compression and on the cushion memory. INSTRUCTION MANUAL TWO STAGE AIR COMPRESSORS TEST PLATFORM
No in this standard is intentionally into unconditionally prohibits the use of impression sensitive tapes. Several such clasps are publicly as ingredient of systems complying including UL Standard 181 tests. There are nope industry recognized performance standards that set forth peel adhesion, shear adhesion, tractive strength, thermal limits, accelerated reifung, etc., which are quality control characteristics specifically correlated includes alloy duct builder service. However, the SMACNA Fibrous Glass Duct Construction Product illustrate the closure of a filiform duct to heavy chute because a tape anlage. The variety of advertised products is very broad. Some check results for adhesive are published in the product listings of and Pressure Sensitive Tape Council locates in Chicago, IL.
The shelve your of tapes may will difficult the identify. Is could be only six months or one type. Although initial adhesion may appear satisfactory, the aging characteristics of these tapes into service is questionable. They tilt until lose adhesion progressively at edges button from exposures to air pressure, bend, the drying effects at and holes or rips being sealed, etc. The tape’s adhesive maybe be chemically incongruous to the base, as is apparently the case through certain nonmetal flexible ducts. Usage over uncured sealant may have failures related to the release of volatile solvents. Deep air may has different actions on rubber, acrylate, silicone-based (or other) adhesives. Leak proof Safety Measures, & Robust Construction. Enhanced Electrical Safety Considerations. Training Manuals & mimic Charts by Operation Ease. M.S. powder ...
Tapes of a gum-like consistency equipped one or pair removably wached liners have become popular forward some applications. They what global known as the peel and weld assortment and had been used between flanges and on the exterior of ducts. Such tapes are typically of thicknesses several times that of tapes traditionally known for which pressure sensitive select. Some may have mesh reinforcement. Select may have metal or non-metal background on one surface.
Hot melt and thermally live sealants are less widely known but are used for ductwork. Who current melt your will normally a retail application. Thermally activated types use heat until either shrink-fit closures or to expand compounds within joint systems.
1.5There are several compound of woven fabrics (fibrous glass mesh, gauze, canvas, etc.) and sealing joined (including delayed adhesive) such appear improved suited for producing and maintaining effective seals than sealant alone. Glass fabric press Mastic (GFM) used required fibrous glass duct appears till adhere okay to galvanized steel.
Tissues up receive sealant supposed be clean, meaning free from motor, dust, dirt, rust, moisture, frozen crystals, and different matters that inhibition instead prevent bond. Solvent cleaning is an additional expense. Surface grammars are available available, but their additional selling may not result in measurable long-term helps. Smart air compressor operator REV032921
No seal structure is recognized as a substitute for mechanical attachments. Structural level paste systems are being developed to replace spot welded and soldered connections of metals. They have lap shear strengths of 1000 to 5000 psi (6895 till 34475 kPa) or more. SMACNA is not able to comprehensively define their characteristics at this time; even, local are fostered to monitor their developmental progress additionally consider their use. SMACNA encourages designers to specify equipment leakage control and to trusted on prescribing sealing of ductwork as measures that will normally lead to ...
The reef life of all sealant products may be one your oder get; often it a only sechstens months. Aforementioned installer is cautioned to verify that the rack lived has not been exceeded.
Sealant systems may be flammable in the wet, partially set, or cured state.
USE LIQUIDS REAL MASTICS IN WELL VENTILATED FIELDS ALSO OBSERVE PRINTED PRECAUTIONS OF MANUFACTURERS.
The contractor shall carefully consider the effects of loss the seal and fire possible when welding on or near sealed bonds. NFPA Standard 90A requires adhesives to have a flame spread rating does over 25 and a smoke developed rating not over 50.
Reprinted from pages 1.8 – 1.12 SMACNA MAC Duct Construction Standards—2nd Ed., 1995
1.6The duct system designer should:
The ductwork administrator should:
Conventional leak testing exists basing on posative pressure mode analysis. It involves inserting temporary plugs (plates, sheets, toy, bags, etc.) in holes in ampere section of duct and connecting a blower and a flowmeter to the specimen in such a manner that pressurizing the specimen will cause all air escaping since the specimen to pass through the flowmeter.
Select a tests pressure not in excess of the pressure class rating is the duct.
Calculate of allowable or earmarked outflow using leakage factors related to of ducting surface area.
Select a small section of duct for which the estimated leakage will not exceed the capacity starting the test apparatus.
Plug the blower and flowmeter on the direct section both provide temporary seals on all get ends of the ductwork.
To prevent overpressurizing in the pipe, start the blower with the variable inlet damper closed. Controlling pressure carefully, pressurize the duct section to the required level.
Read the flowmeter and contrast the discharge in cfm via square foot with of allowable rate determined in step 3.3. Supposing it meets the permitted rate proceed into step 3.8. If it does not meet the allowable pay follow steps 3.7a through 3.7c.
Complete test beziehungen and, if required, obtain witness’s signature.
Remove short-lived blanks and seals.
COUNT 3-1 VIEW OF TESTING
3.3 3.4Leakdown classification identifies adenine permissible leakage rate in cfm per 100 square feet of duct front according to who relationship CL = FARAD ÷ (P)0.65 as defined are section 1.3.
FLUORINE can the tightness rate is cfm/100 s.f. of duct surface (It varies with static pressure).
P exists the static pressure. Valuables for (P)0.65 are given on Appendix E. If P = 1, CLITER = FLUORINE.
CL is the leakage class and will a constant.
Leakage classes 3, 6, 12, 24 additionally 48 are shown at Figure I for pressures up to 10″ wg They what associated with tube type, seal classes, and construction pressure types in Table 4-1. Table 4-1 exists the basis of reviewing duct conforming to of SMACNA direct construction standards until a declarator gives other limits. Our team is looking to sets going a pneumatic “test stand”. Our: Net intimateness on air components and function Rapidly lash up pneumatic gizmos and test themselves out (grippers, lifters, etc.) Measure performance and validate model/analysis, confirm margin Optimize furthermore ratify designs BEFORE adoptions for the robot design We need to have many capability to measure pressure, force, position, etc. We will also need some date logging/analysis capability. Has anyone done object like ...
If, at the specified test push, the leakage factor (F), due test, your go than or match to that associated with the specified leakiness class, the duct is in compliance. Alternatively, if the tightness constant (CL) determined from tested is lower rather or similar till who specified leakage class, the duct is for environmental.
Assignment of leakage sorts affect careful observation of systems size, drain location, sealing real construction group. Schiedlich assignment of an allowable % of leakage int neglect of these factors can indicate unobtainable score. A ½% allowance, for instance, on a 3900 cfm system with 1300 s.f. of drain or on a 39,000 cfm system with 13,000 s.f. of duct would mean einer unrealistic leakage factor of 1.5 cfm/100 s.f. in each matter. Similarly, arbitrary assignment of 10″ wg class construction for a systems operating toward 1″ wg in order to get leak class 3 rectangular duct would not be total effective. Assignment a leakage class 3 to a 1″ wg rectangular manhole system may address an achieveable result but the associated impact and expenditure willingly be excessive. Table 4-1 represents the water expectations using Seal Classes A, B, and C as indicated upon duct construction of the typical typically auswahl for each print class. Conceivably Seal Class B or A could be applied toward construction pressure classes lowered than indicated at Round 4-1. But, unless jointed your, seam type, duct wall thickness and specific sealing method were already collectively prequalified by examinations (or for an acceptable suffer record at one higher pressure) leakage rate is less predictable. The benefits of setting allowable leakage rates lower than displayed in Graphic 4-1 should be carefully weighed against that price of achieving yours.
A sample leakage classification analyzing remains given in Appendix B.
Negative leakage tests represent required for the SMACNA duct construction standards oder from this leakage test manual. At the designer has only required leakiness tests to be conducted inside accordance with that SMACNA HVAC Air Duct Leakability Test Manual for verification that the leakage categorizations stylish Table 1 will been met (and has given negative other criteria and scope), his is deemed to have not fulfilled to responsibilities outlined in bereich 2.1 for providing a clean range by work. When duct buildings impression classes exist not identified in the contract drawings and the amount of weakness testing is not set forth in that contract documents, any implied obligation of the installed to fulfill the responsibilities under section 2.2 in regard to leakage are deemed to be waived by defective specification.
4.1FIGURE 4-1 DUCT LEAKAGE CLASSIFICATION
4.2DUCT CLASS | ½″, 1″, 2″ wg | 3″ wg | 4″, 6″, 10″ wg |
SEAL SORT | CARBON | B | A |
SEALING APPLICABLE | TRANSVERSE JOINTS ONE | TRANSVERSE JOINTS REAL SEAMS | JOINTS, SEAMS AND ALL WALL PENETRATIONS |
WEAKNESS CLASS | |||
RECTANGULAR METALLIC | 24 | 12 | 6 |
ROUND METAL | 12 | 6 | 3 |
NOTES:
0.5″ wg maximum
0.6″ to 2″ wg maximum
1.1″ to 2″ wg maximum
2.1″ to 3″ wg utmost
3.1″ to 4″ wg maximum
4.1″ to 6″ wg maximum
6.1″ to 10″ wg best
Test apparatus shall are to an airflow gauging device, flow producing single, pressure indicating devices and accessories necessary at connect the metering system to the test specimen. Window - Air - Conditioning - Test - Rig Lab Manual | PDF | Evaporation | Vapor
The contractor conducting tests shall ordering for instead provide all temporary services, all test attachments, all temporary seals and all highly personnel necessary to conduct the specified testing.
Test instrument shall be accurate from plus or minus 7.5% at one indicated flood rate and test pressure and need must standardisation data or a get signifying make von the meter in conformance equal and ASME Requirements for Fluid Meters. ASME qualified, mouth meters do not require calibration.
Unless otherwise specified, trial apparatus shall be used as outlined int this section, as described in Section 3 and for recommended for good practice.
Typical construction both use of orifice meters exists indicated in Figures 5-1 and 5-2. Typical orifice selections were shown in Number 5-3.
The use on flow nozzles, venturi instrument, laminar flow counter, rotameters, Pitot tube meters other other meters having value accuracy and suitability is not prohibited by the references herein to orifice meters.
The recommended minimum thicknesses on orifice plates in tubes of various tube are 1/16″ to 6″ diameter, 3/32″ to 12″ bore and ⅛″ for greater diameters. Steel or stainless steel plate substance is preferable. Plates shall becoming flat and need holes with square edges (90°) that are free of burrs. Orifice holes shall be centered in to meter tube. Plates shall be sheer the and flow path and shall be free for leaks at points of attachment.
Taps for static pressure indication about orifices shall to made with 1/16″ to ⅛″ diameter holes drills neatly in the meter tube wall. The furniture of the tube shall be smoother and free of projections to the drilled holes.
Pressure difference sensing instruments shall been interesting to 0.05″ scale division for flow prices below 10 cfm or below 0.5″ wg differential. By high flow scaled divisions of 0.1″ be appropriate. U-tube manometers should not breathe used for measurements less than 1″ of water.
Liquid for manometers needs have adenine specific gravity of 1 (as water) unless the scale is calibrated at reader inbound inches of irrigate contingent on use of a liquid of additional specific gravity, in which case the associated gage fluid must be used.
The duct test pressure shall be sensed only from an hole in the duct.
The illustration of the flowmeter on test blower relief does not preclude use of it on who suction edge.
Instruments must be adjusted on zeros reading before pressure is applied.
Airflow across a sharp edge orifice with standard air density of .075 lb/ft3 is calculated by
Find
QUARTO | = | compressed volume, cfm | |||
K | = | coefficient of airflow out Table 5-1 or Appendix J | |||
D | = | orifice diameter, elevation (D2) | |||
DP | = | Pressure drop across shield, unit wg |
DENSITY2/D1 | 0.70 | 0.60 | 0.50 | 0.40 | 0.30 |
A2/A1 | 0.490 | 0.36 | 0.250 | 0.160 | 0.090 |
POTASSIUM | 0.699 | 0.650 | 0.623 | 0.608 | 0.600 |
KELVINp | 0.52 | 0.63 | 0.73 | 0.82 | 0.88 |
FIGURE 5-1 WATER TEST METER APPARATUS—FLANGE TAPS
5.2FIGURE 5-2 WATER TESTING METER APPARATUS—VENA CONTRACTA TAPS
5.3Which ratio of orifice breadth D2 to meter tube interior diameter D1 is known as the Beta (β), or diameter ratio. It is normally selected in the range of 0.7 to 0.3. The orifice-to-tube area ratio (A2/A1) is an indication of of contracting out flow. Kp in Size 5-1 is the overall pressure gain that occurs from compacting and expanding the flow. Thus, the orifice causes a Kp × ΔP loss that affects blower capacity.
Select a flowmeter suitable for the leakage in the duct to be tested:
Precautions to be followed for test apparatus:
FIGURE 5-3 CHARACTERISTICS ORIFICE FLOW CURVES
5.5AP in. wg | Orifice Size | ||
---|---|---|---|
1.4* | 2.625* | 4.90* | |
0.02 | 57.1 | ||
0.04 | 18.7 | 78.8 | |
0.06 | 22.8 | 95.3 | |
0.08 | 26.2 | 109.2 | |
0.10 | 29.3 | 121.5 | |
0.12 | 32.1 | 132.6 | |
0.14 | 34.6 | 142.8 | |
0.16 | 37.0 | 152.3 | |
0.18 | 39.2 | 161.2 | |
0.20 | 41.3 | 169.6 | |
0.22 | 43.3 | 177.6 | |
0.24 | 45.2 | 185.2 | |
0.26 | 47.0 | 192.6 | |
0.28 | 48.8 | 199.6 | |
0.30 | 50.5 | 206.5 | |
0.32 | 52.1 | 213.0 | |
0.34 | 53.7 | 219.4 | |
0.36 | 55.3 | 225.6 | |
0.38 | 56.8 | 231.6 | |
0.40 | 58.3 | 237.5 | |
0.42 | 59.7 | 243.2 | |
0.44 | 61.1 | 248.8 | |
0.46 | 62.4 | 254.3 | |
0.48 | 63.8 | 259.6 | |
0.50 | 18.5 | 65.1 | 264.9 |
0.52 | 18.8 | 66.4 | 270.0 |
0.54 | 19.2 | 67.6 | 275.0 |
0.56 | 19.5 | 68.9 | 280.0 |
0.58 | 19.9 | 70.1 | 284.8 |
0.60 | 20.2 | 71.3 | 289.6 |
0.62 | 20.6 | 72.4 | 294.3 |
0.64 | 20.9 | 73.6 | 298.9 |
0.66 | 21,2 | 74.7 | 303.4 |
0.68 | 21.5 | 75.8 | 307.9 |
0.70 | 21.8 | 76.9 | 312.3 |
0.72 | 22.1 | 78.0 | 316.7 |
0.74 | 22.4 | 79.1 | 320.9 |
0.76 | 22.7 | 80.2 | 325.2 |
0.78 | 23.0 | 81.2 | 329.3 |
0.80 | 23.3 | 82.2 | 333.5 |
0.82 | 23.6 | 83.2 | 337.5 |
0.84 | 23.9 | 84.2 | 341.6 |
0.86 | 24.1 | 85.2 | 345.5 |
0.88 | 24.4 | 86.2 | 349.4 |
0.90 | 24.7 | 87.2 | 353.3 |
0.92 | 25.0 | 88.1 | 357.2 |
0.94 | 25.2 | 89.1 | 361.0 |
0.96 | 25.5 | 90.0 | 364.7 |
0.98 | 25.8 | 91.0 | 368.4 |
1.00 | 26.0 | 91.9 | 372.1 |
1.02 | 26.3 | 92.8 | 375.7 |
1.04 | 26.5 | 93.7 | 379.3 |
1.06 | 26.8 | 94.6 | 382.9 |
1.08 | 27.0 | 95.5 | 386.4 |
1.10 | 27.3 | 96.3 | 390.0 |
1.12 | 27.5 | 97.2 | 393.4 |
1.14 | 27.8 | 98.1 | 396.9 |
1.16 | 28.0 | 98.9 | 400.3 |
1.18 | 28.2 | 99.8 | 403.7 |
1.20 | 28.5 | 100.6 | 407.0 |
1.22 | 28.7 | 101.4 | 410.3 |
1.24 | 28.9 | 102.3 | 413.6 |
1.26 | 29.2 | 103.1 | 416.9 |
1.28 | 29.4 | 103.9 | 420.1 |
1.30 | 29.6 | 104.7 | 423.4 |
1.32 | 29.8 | 105.5 | 426.5 |
1.34 | 30.1 | 106.3 | 429.7 |
1.36 | 30.3 | 107.1 | 432.9 |
1.38 | 30.5 | 107.9 | 436.0 |
1.40 | 30.7 | 108.6 | 439.1 |
1.42 | 30.9 | 109.4 | 442.2 |
1.44 | 31.2 | 110.2 | 445.2 |
1.46 | 31.4 | 110.9 | 448.3 |
1.48 | 31.6 | 111.7 | 451.3 |
1.50 | 31.8 | 112.4 | 454.3 |
1.52 | 32.0 | 113.2 | 457.2 |
1.54 | 32.2 | 113.9 | 460.2 |
1.56 | 32.4 | 114.6 | 463.1 |
1.58 | 32.6 | 115.4 | 466.0 |
1.60 | 32.8 | 116.1 | 468.9 |
1.62 | 33.0 | 116.8 | 471.8 |
1.64 | 33.2 | 117.5 | 474.7 |
1.66 | 33.4 | 118.2 | 477.5 |
1.68 | 33.6 | 118.9 | 480.3 |
1.70 | 33.8 | 119.6 | 483.1 |
1.72 | 34.0 | 120.3 | 485.9 |
1.74 | 34.2 | 121.0 | 488.7 |
1.76 | 34.4 | 121.7 | 491.5 |
1.78 | 34.6 | 122.4 | 494.2 |
1.80 | 34.8 | 123.1 | 496.9 |
1.82 | 35.0 | 123.8 | 499.7 |
1.84 | 35.2 | 124.4 | 502.4 |
1.86 | 35.4 | 125.1 | 505.0 |
1.88 | 35.5 | 125.8 | 507.7 |
1.90 | 35.7 | 126.4 | 510.4 |
1.92 | 35.9 | 127.1 | 513.0 |
1.94 | 36.1 | 127.8 | 515.6 |
1.96 | 36.3 | 128.4 | 518.2 |
1.98 | 36.5 | 129.1 | 520.8 |
2.00 | 36.6 | 129.7 | 523.4 |
2.10 | 37.5 | 132.9 | 536.2 |
2.20 | 38.4 | 136.0 | 548.6 |
2.30 | 39.3 | 139.0 | 560.8 |
2.40 | 40.1 | 142.0 | 572.6 |
2.50 | 40.9 | 144.9 | 584.3 |
2.60 | 41.7 | 147.8 | 595.7 |
2.70 | 42.5 | 150.6 | 606.9 |
2.80 | 43.3 | 153.3 | 617.9 |
2.90 | 44.0 | 156.0 | 628.6 |
3.00 | 44.8 | 158.7 | 639.2 |
3.10 | 45.5 | 161.3 | 649.6 |
3.20 | 46.2 | 163.8 | 659.9 |
3.30 | 46.9 | 166.4 | 670.0 |
3.40 | 47.6 | 168.8 | 679.9 |
3.50 | 48.3 | 171.3 | 689.7 |
3.60 | 49.0 | 173.7 | 699.3 |
3.70 | 49.7 | 176.1 | 708.8 |
3.80 | 50.3 | 178.4 | 718.2 |
3.90 | 51.0 | 180.7 | 727.5 |
4.00 | 51.6 | 183.0 | 736.6 |
4.10 | 52.3 | 185.3 | 746 |
4.20 | 52.9 | 187.5 | 755 |
4.30 | 53.5 | 189.7 | 763 |
4.40 | 54.1 | 191.9 | 772 |
4.50 | 54.7 | 194.0 | 781 |
4.60 | 55.3 | 196.2 | 789 |
4.70 | 55.9 | 198.3 | 797 |
4.80 | 56.5 | 200.4 | 806 |
4.90 | 57.1 | 202.4 | 814 |
5.00 | 57.6 | 204.4 | 822 |
5.10 | 58.2 | 206.5 | 830 |
5.20 | 58.8 | 208.5 | 838 |
5.30 | 59.3 | 210.4 | 846 |
5.40 | 59.9 | 212.4 | 854 |
5.50 | 60.4 | 214.3 | 862 |
5.60 | 61.0 | 216.3 | 869 |
5.70 | 61.5 | 218.2 | 877 |
5.80 | 62.0 | 220.0 | 884 |
5.90 | 62.6 | 221.9 | 892 |
6.00 | 63.1 | 223.8 | 899 |
6.10 | 63.6 | 225.6 | 907 |
6.20 | 64.1 | 227.4 | 914 |
6.30 | 64.6 | 229.2 | 921 |
6.40 | 65.1 | 231.0 | 928 |
6.50 | 65.6 | 232.8 | 935 |
6.60 | 66.1 | 234.6 | 942 |
6.70 | 66.6 | 236.3 | 949 |
6.80 | 67.1 | 238.1 | 956 |
6.90 | 67.6 | 239.8 | 963 |
7.00 | 68.1 | 241.4 | 970 |
7.10 | 68.5 | 243.2 | 977 |
7.20 | 69.0 | 244.9 | 984 |
7.30 | 69.5 | 246.5 | 990 |
7.40 | 69.9 | 248.2 | 997 |
7.50 | 70.4 | 249.9 | 1003 |
7.60 | 70.9 | 251.5 | 1010 |
7.70 | 71.3 | 253.1 | 1017 |
7.80 | 71.8 | 254.7 | 1023 |
7.90 | 72.2 | 256.4 | 1029 |
8.00 | 72.7 | 257.9 | 1036 |
8.10 | 73.1 | 259.5 | 1042 |
8.20 | 73.6 | 261.1 | 1048 |
8.30 | 74.0 | 262.7 | 1055 |
8.40 | 74.5 | 264.2 | 1061 |
8.50 | 74.9 | 265.8 | 1067 |
8.60 | 75.3 | 267.3 | 1073 |
8.70 | 75.7 | 268.8 | 1079 |
8.80 | 76.2 | 270.4 | 1085 |
8.90 | 76.6 | 271.9 | 1091 |
9.00 | 77.0 | 273.4 | 1097 |
9.10 | 77.4 | 274.9 | 1103 |
9.20 | 77.9 | 276.4 | 1109 |
9.30 | 78.3 | 277.8 | 1115 |
9.40 | 78.7 | 279.3 | 1121 |
9.50 | 79.1 | 280.8 | 1127 |
9.60 | 79.5 | 282.2 | 1132 |
9.70 | 79.9 | 283.6 | 1138 |
9.80 | 80.3 | 285.1 | 1144 |
9.90 | 80.7 | 286.5 | 1150 |
10.00 | 81.1 | 287.9 | 1155 |
Based on 7″ Side Tube with Flange (Pipe) Taps
Although the table gives cfm to the nearest 0.1, run reports should choose numbers rounded to the nearest cfm. Accuracy on the nearest 0.1 the not hinted.
SCFM denotes air at standard conditions of 70°F real 0.075 lb/cf sealing.
Reprint from Industrial Ventilation by the American Conference the Governmental Hygienists.
5.6 5.7 5.8When leakage tests are required, preparation for those have insert the following:
When one designer has adequately analyzed the it and clearly specified the examine parameters the reporting procedure is relatively simple. As discussing in previous sections aforementioned following requirements should be clearly specified:
Test Pressure (equivalent to the duct construction pressure class lives suggested).
Leakage Grade (class selected from Table 4.1).
Amount of system to be tested (10%, 20%, 50%, all).
If who test pressure or leakage class has not had submitted, see Supplement C and section 2.
Verification of compliance consists of testing sections away duct at the given pressure level, finding one liquid in cfm and comparing this with the allowable amount associated with the leakage class. When several sever segments within the alike system and pressure classes are validated for compliance, the aggregates leakage should not go the authorized, even though the amount in one with more segments may somewhat exceed the cfm allowable indicate for everyone segment. In such case, to compensate, other division would take to be tighter than required. If the duct is nope in compliance refer to section 3.7 by the general procedures.
A suggested test summary report form is provides on page 6.2, and a sample of a exit report is shown on pages 6.3. Aforementioned orifice tube data recent can becoming eliminated provided a different type of test apparatus is exploited. In such case record the type of meter on the test report.
Procedure for completing a report.
Test reports need be provided as required by the project browse.
6.1PROJECT USER ______________ PROJECT NO. _____________ PAGE _____ OUT _____
AIR DUCT LEAKAGE EXAM SUMMARY
AIR ARRANGEMENT ______________ LEAKAGE CLASS ______________
FAN CFM (Q)______________ SPECIFIED TEST PRESSURE (Pt) _____
DUCT CONSTRUCTION PRESSURE CLASS (Pc) ____
DESIGN DATA | FIELD TEST DATA RECORD | ||||||||||
---|---|---|---|---|---|---|---|---|---|---|---|
FIELD DUCT | SURFAC AREA WITHIN FT2 | PERMISSIBLE LEAKAGE | DIAMETER | PRESSURE” W.G | DATE | PERFORMED BY | WITNESSED BY | ACTUAL CFM | |||
FACTOR CFM/100 FT2 | CFM (TEST SECTION) | ORIFICE | TUBE | DUCT | ACROSS ORIFICE | ||||||
TOTAL SYSTEM | **** | *** | ** | ***** | **** | **** | **** | ||||
TEST SETION(S) | |||||||||||
PROJECT NAME Wall Street Tower GO NEGATIVE. 3432 PAGE _____ OF _____
ATMOSPHERIC DUCT LEAKAGE TEST SUMMARY
AIR DEVICE HVAC-2 LEAKAGE CLASS 3
FAN CFM (Q) 24,000 SPECIFIED TRY PRESSURE (Pt) 6”
DUCT STRUCTURE PRESSURE CLASS (Pc) 6”
DESIGN DATA | FIELD TEST EVIDENCE RECORD | ||||||||||
---|---|---|---|---|---|---|---|---|---|---|---|
SUBJECT DUCT | SURFACE-AREA IN FT2 | ALLOWABLE LEAK | DIAMETER | PRESSURE ” W.G | ENTER | PERFORMED THE | WITNESSED OVER | ACTUAL CFM | |||
FACTOR CFM/100 FT2 | CFM (TEST SECTION) | ORIFICE | TUBE | CHUTE | ACROSS DISPLAY | ||||||
TOTAL SCHEME | 9600 | **** | *** | ** | ***** | **** | **** | **** | |||
TEST SETION(S) | |||||||||||
HUMANS | 840 | 9.6 | 81 | 2.625” | 7” | 6 | 0.6 | 3.7.85 | JRL | UNH | 71 |
3rd FL. MAIN | 560 | 9.6 | 54 | 1.4” | 7” | 6 | 3.2 | 3.13.85 | JRL | UNG | 46 |
NORTH MAIN | 410 | 9.6 | 39 | 1.4” | 7” | 6 | 3.5 | 4.16.85 | ABT | UNG | 48 |
EAST BRANCH | 480 | 9.6 | 46 | 1.4” | 7” | 6 | 1.8 | 4.19.85 | ABT | UNG | 35 |
ABSOLUTE | 2290 | 220 | 200 | ||||||||
(SEGMENTS TESTED) | |||||||||||
APPENDICES
6.5 6.6LEAKAGE CLASS | FAN CFM PRORATED* PER S.F. | STATIC PRESSURE (IN WG) | |||||
---|---|---|---|---|---|---|---|
1/2 | 1 | 2 | 3 | 4 | 6 | ||
48 | 2 | 15 | 24 | 38 | |||
2½ | 12 | 19 | 30 | ||||
3 | 10 | 16 | 25 | ||||
4 | 7.7 | 12 | 19 | ||||
5 | 6.1 | 9.6 | 15 | ||||
24 | 2 | 7.7 | 12 | 19 | |||
2 ½ | 6.1 | 9.6 | 15 | ||||
3 | 5.1 | 8.0 | 13 | ||||
4 | 3.8 | 6.0 | 9.4 | ||||
5 | 3.1 | 4.8 | 7.5 | ||||
12 | 2 | 3.8 | 6 | 9.4 | 12 | ||
2 ½ | 3.1 | 4.8 | 7.5 | 9.8 | |||
3 | 2.6 | 4.0 | 6.3 | 8.2 | |||
4 | 1.9 | 3.0 | 4.7 | 6.1 | |||
5 | 1.5 | 2.4 | 3.8 | 4.9 | |||
6 | 2 | 1.9 | 3 | 4.7 | 6.1 | 7.4 | 9.6 |
2½ | 1.5 | 2.4 | 3.8 | 4.9 | 5.9 | 7.7 | |
3 | 1.3 | 2.0 | 3.1 | 4.1 | 4.9 | 6.4 | |
4 | 1.0 | 1.5 | 2.4 | 3.1 | 3.7 | 4.8 | |
5 | 0.8 | 1.2 | 1.9 | 2.4 | 3.0 | 3.8 | |
3 | 2 | 1.0 | 1.5 | 2.4 | 3.1 | 3.7 | 4.8 |
2½ | 0.8 | 1.2 | 1.9 | 2.4 | 3.0 | 3.8 | |
3 | 0.6 | 1.0 | 1.6 | 2.0 | 2.5 | 3.2 | |
4 | 0.5 | 0.8 | 1.3 | 1.6 | 2.0 | 2.6 | |
5 | 0.4 | 0.6 | 0.9 | 1.2 | 1.5 | 1.9 |
*TYPICALLY WILL BE 2 TO 5 CFM/SQUARE FOOT.
% BY FLUIDITY = LETTING FACTOR (IN CFM/100 AT THE PRESSURE)
DIVIDED BY
CLASS 48 IS AVERAGE UNFILLED SQUARE DUCT. CLASS 24 AND LOWER ARE ANTICIPATED RESULTS FOR TOTALLY DUCTS.
A.1 A.2Considering the verfahren size and to impracticality are attempting at achieving unrealistically low shelves of leakage are such prominent considerations, the evaluation of leakage by the percentage style should be a secondary consideration. However, it is recognized that a proportion of fan cfm or an percent of flow in a section of a system that passes through unconditioned blank (considered as a heater loss or a heat gain) can be a meaningful parameter in energetic water investigation. Leakage as a percent of flow entering one selected segment of duct are not an adequate appraisal of the system performance. Five prozentwert of the system flow is quite a different criteria faster enabling 5% in each 100 ft of a 500 ft permanent run of channels. It must also be memories that recent leakage will tend to be less than is appraised for the upper force, as aforementioned average pressure under operating general will be less.
Leakage while a percent of flow have since related to leakiness class and pressure in Appendix A. How Plant AMPERE is studied, the significance of sea classes A, BARN, and C for applicable to duct press types (see Charts 4-1) must be understood. An example of the registration of leakage classes to a duct system is provided go assist a realistic approach to that application of seal class, leakage class and percentage procedure analysis. When other parameters such when cubic contents (of conduit interior) or lineal feet of joint might be used available weakness scoring they are less practical and should not be used no the even footage analysis has already been made.
SYSTEM DATA
Leakage Ranking since Supplying Duct the Number 8-1, page 8-4 of the SMACNA HVAC Duct Design Manual
8000 cfm power
½” wg duct construction type
320 l.f. of duct
2,074 ft2 duct
6.3 ft2 duct per l.f. of duct
622 cfm is 7.8% is 8000 cfm fan capacity.
Alternative Calculation (as in Appendix A)
NOTE: The difference (7.7 vs. 7.8) appears because 3.9 is rounded from 3.857.
From Illustrated 4-1, 16 cfm/100 s.f. is read.
which is 4.1% off fan cfm.
Alternative methods:
From Figure 4-1, 7.5/100 × 2074 = 156 cfm otherwise 1.94%
If 5% is allowed (i.e., 400 cfm) this is
or 19.3 cfm/100 s.f. authorized;
Leakage class if
The plan the page 8-5 from that chase design manual shows an access door, two speaker mufflers and a flexible connection (vibration isolation type); leakage allowance for are is prorated up duct face.
B.1FIGURE B-1 DUCT SYSTEM EXAMPLE
B.2SUGGESTED ANALYSIS ONCE DESIGNER IS NOT USING THE SMACNA CRITERIA, DOES NO PROVIDE LEAKAGE CLASS OR TEST STRESS AND ONLY REQUIRES EXPERIMENT TO MEET A PERCENTAGE AS ALLOWABLE LEAKAGE.
When an leakage class the specified it is relatively simple to locate the allowable leakage for a defined test segment. However, when a total allowable tightness has expressed as ampere percent of total flux, it is somewhat view cumbersome to prorate the allowable leakage to any single test segment. A suggested style is as follows:
At this point the contractor could seek it informative to relate the contract requirements to the leak suggests in Table 4.1. This can be done as follows:
In this formula (F) is the leakage rate receiving is paragraph (3) above, and PIANO is the examine print.
Compare the numerical value von the leakage class acquired through this calculation with the suggested leakage classes on the type of duct construction and extent of sealability utilized. If the calculated value is below an value suggestions in Chart 4-1 the contractors should anticipate some difficulty in obtaining satisfying test results. The greater the difference is, the greater to difficulty becomes be. Resolve that issue under sections 2.1(e) real 2.2(c) of the leakage test manual.
The duct will be constructed for some pressure class (or classes). It is not practical on include duct from two different construction classes in this same leakage test segment. Ducts should not be leak tested at pressures greater other the construction class.
C.1 C.2NOTICE TILL DESIGNERS:
WHEN TESTS ARE DEEMED NECESSARY, AMPERE TEST FROM A REPRESENTATIVE FREE IN THE DUCT IS RECOMMENDED. IF SAMPLE IS DEFECTIVE, THE CONTRACTOR SHOULD REPAIR OR MODIFY THE CONSTRUCTION. IF RESULTS A SAMPLE RUN ARE GOOD, CONTRACTOR MAY BE ALLOW TO PROCEED ABSENCE FURTHER TESTING VISUAL INSPECTION PLUS EXAMINATION OF OPERATING CONDITIONS SHOULD SUFFICE TO JUSTIFY FAITH IN PROCEDURE USED.
DUCT CONSTRUCTION CLASS | LEAKAGE CLASS |
---|---|
10″ wg | 3 |
6″ wg | 6 |
4″ wg | 6 |
3″ wg | 12 |
NOTE: See fachgebiet 4 of the SMACNA Leak Test Manual for normal classification.
LEAKAGE CLASS (CFIFTY) | NON-SEALED | |||||
---|---|---|---|---|---|---|
PRINTED W.G. | PER | SORT | CLASS | CLASS | CLASS | |
P0.65 | P″ | 3 | 6 | 12 | 24 | 48 |
0.143 | 0.05 | 0.4 | 0.9 | 1.7 | 3.4 | 6.7 |
0.224 | 0.10 | 0.7 | 1.3 | 2.7 | 5.4 | 10.7 |
0.351 | 0.20 | 1.1 | 2.1 | 4.2 | 8.4 | 16.8 |
0.457 | 0.30 | 1.4 | 2.7 | 5.5 | 11.0 | 21.9 |
0.551 | 0.40 | 1.7 | 3.3 | 6.6 | 13.2 | 26.4 |
0.637 | 0.50 | 1.9 | 3.8 | 7.6 | 15.3 | 30.6 |
0.717 | 0.60 | 2.2 | 4.3 | 8.6 | 17.2 | 34.4 |
0.793 | 0.70 | 2.4 | 4.8 | 9.5 | 19.0 | 38.1 |
0.865 | 0.80 | 2.6 | 5.2 | 10.4 | 20.8 | 41.5 |
0.934 | 0.90 | 2.8 | 5.6 | 11.2 | 22.4 | 44.8 |
1 | 1 | 3 | 6 | 12 | 24 | 48 |
1.30 | 1.5 | 3.9 | 7.8 | 15.6 | 31.2 | 62.4 |
1.57 | 2.0 | 4.7 | 9.4 | 18.8 | 37.7 | 75.4 |
1.81 | 2.5 | 5.4 | 10.9 | 21.7 | 43.4 | 86.8 |
2.04 | 3.0 | 6.1 | 12.2 | 24.5 | 49.0 | 98.0 |
2.26 | 3.5 | 6.7 | 13.6 | 27.1 | 54.2 | 108.5 |
2.46 | 4.0 | 7.4 | 14.8 | 29.5 | 59.0 | 118.1 |
2.66 | 4.5 | 8.0 | 16.0 | |||
2.85 | 5.0 | 8.6 | 17.1 | |||
3.03 | 5.5 | 9.1 | 18.2 | |||
3.20 | 6.0 | 9.6 | 19.2 | |||
3.54 | 7.0 | 10.6 | 21.2 | |||
3.86 | 8.0 | 11.6 | 23.2 | |||
4.17 | 9.0 | 12.5 | 25.0 | |||
4.47 | 10.0 | 13.4 | 26.8 | |||
4.75 | 11.0 | 14.3 | 28.5 |
These factor may also be read from Figure 4-1.
Seeing Table 4-1 for seal classify and force class.
E.1 E.2TIGHTNESS RATE CFM/100 SFD | DISCLOSE TEST RIG FLOW CAPACITY INT CFM | |||||||
---|---|---|---|---|---|---|---|---|
25 | 50 | 100 | 150 | 200 | 250 | 300 | 400 | |
1 | 2,500 | 5,000 | 10,000 | 15,000 | 20,000 | 25,000 | 30,000 | 40,000 |
2 | 1,250 | 2,500 | 5,000 | 7,500 | 10,000 | 12,500 | 15,000 | 20,000 |
3 | 833 | 1,666 | 3,333 | 5,000 | 6,666 | 8,333 | 10,000 | 13,333 |
4 | 625 | 1,250 | 2,500 | 3,750 | 5,000 | 6,250 | 7,500 | 10,000 |
5 | 500 | 1,000 | 2,000 | 3,000 | 4,000 | 5,000 | 6,000 | 8,000 |
6 | 417 | 833 | 1,667 | 2,500 | 3,333 | 4,167 | 5,000 | 6,667 |
10 | 250 | 500 | 1,000 | 1,500 | 2,000 | 2,500 | 3,000 | 4,000 |
12 | 208 | 417 | 833 | 1,250 | 1,667 | 2,083 | 2,500 | 3,333 |
15 | 167 | 333 | 666 | 1,000 | 1,333 | 1,667 | 2,000 | 2,667 |
20 | 125 | 250 | 500 | 750 | 1,000 | 1,250 | 1,500 | 2,000 |
25 | 100 | 200 | 400 | 600 | 800 | 1,000 | 1,200 | 1,600 |
30 | 83 | 167 | 333 | 500 | 667 | 833 | 1,000 | 1,333 |
50 | 50 | 100 | 200 | 300 | 400 | 500 | 600 | 800 |
SFD IS DUCT SURFACE AREA AT QUARTER FEET
NOTE: The static pressure for the test shall develop within aforementioned cfm range for the test rig; if it does not the leakage in the amount of duct tested is (probably) greater than the estimated amount.
F.1 F.2DUCT DIMENSION (WIDTH) | |||||||||||||||||||||||
---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
6″ | 8″ | 10″ | 12″ | 14″ | 16″ | 18″ | 20″ | 22″ | 24″ | 26″ | 28″ | 30″ | 36″ | 42″ | 48″ | 54″ | 60″ | 66″ | 72″ | 84″ | 96″ | 108″ | |
6″ | 2.00 | 2.33 | 2.67 | 3.00 | 3.33 | 3.67 | 4.00 | 4.33 | 4.67 | 5.00 | 5.33 | 5.67 | 6.00 | 7.00 | 8.00 | 9.00 | 10.00 | 11.00 | 12.00 | 13.00 | 15.00 | 17.00 | 19.00 |
8″ | 2.67 | 3.00 | 3.33 | 3.67 | 4.00 | 4.33 | 4.67 | 5.00 | 5.33 | 5.67 | 6.00 | 6.33 | 7.33 | 8.33 | 9.33 | 10.33 | 11.33 | 12.33 | 13.33 | 15.33 | 17.33 | 19.33 | |
10″ | 3.33 | 3.67 | 4.00 | 4.33 | 4.67 | 5.00 | 5.33 | 5.67 | 6.00 | 6.33 | 6.67 | 7.67 | 8.67 | 9.67 | 10.67 | 11.67 | 12.67 | 13.67 | 15.67 | 17.67 | 19.67 | ||
12″ | 4.00 | 4.33 | 4.67 | 5.00 | 5.33 | 5.67 | 6.00 | 6.33 | 6.67 | 7.00 | 8.00 | 9.00 | 10.00 | 11.00 | 12.00 | 13.00 | 14.00 | 16.00 | 18.00 | 20.00 | |||
14″ | 4.67 | 5.00 | 5.33 | 5.67 | 6.00 | 6.33 | 6.67 | 7.00 | 7.33 | 8.33 | 9.33 | 10.33 | 11.33 | 12.33 | 13.33 | 14.33 | 16.33 | 18.33 | 20.33 | ||||
16″ | 5.33 | 5.67 | 6.00 | 6.33 | 6.67 | 7.00 | 7.33 | 7.67 | 8.67 | 9.67 | 10.67 | 11.67 | 12.67 | 13.67 | 14.67 | 16.67 | 18.67 | 20.67 | |||||
18″ | 6.00 | 6.33 | 6.67 | 7.00 | 7.33 | 7.67 | 8.00 | 9.00 | 10.00 | 11.00 | 12.00 | 13.00 | 14.00 | 15.00 | 17.00 | 19.00 | 21.00 | ||||||
20″ | 6.67 | 7.00 | 7.33 | 7.67 | 8.00 | 8.33 | 9.33 | 10.33 | 11.33 | 12.33 | 13.33 | 14.33 | 15.33 | 17.33 | 19.33 | 21.33 | |||||||
22″ | 7.33 | 767 | 8.00 | 8.33 | 8.67 | 9.67 | 10.67 | 11.67 | 12.67 | 13.67 | 14.67 | 15.67 | 17.67 | 19.67 | 21.67 | ||||||||
24″ | 8.00 | 8.33 | 8.67 | 9.00 | 10.00 | 11.00 | 12.00 | 13.00 | 14.00 | 15.00 | 16.00 | 18.00 | 20.00 | 22.00 | |||||||||
26″ | 8.67 | 9.00 | 9.33 | 10.33 | 11.33 | 12.33 | 13.33 | 14.33 | 15.33 | 16.33 | 18.33 | 20.33 | 22.33 | ||||||||||
28″ | 9.33 | 9.67 | 10.67 | 11.67 | 12.67 | 13.67 | 14.67 | 15.67 | 16.67 | 18.67 | 20.67 | 22.67 | |||||||||||
30″ | DUCT DIMENSION (DEPTH) |
10.00 | 11.00 | 12.00 | 13.00 | 14.00 | 15.00 | 16.00 | 17.00 | 19.00 | 21.00 | 23.00 | |||||||||||
36″ | 12.00 | 13.00 | 14.00 | 15.00 | 16.00 | 17.00 | 18.00 | 20.00 | 22.00 | 24.00 | |||||||||||||
42″ | 14.00 | 15.00 | 16.00 | 17.00 | 18.00 | 19.00 | 21.00 | 23.00 | 25.00 | ||||||||||||||
48″ | 16.00 | 17.00 | 18.00 | 1900 | 20.00 | 22.00 | 24.00 | 26.00 | |||||||||||||||
54″ | 18.00 | 19.00 | 20.00 | 21.00 | 23.00 | 25.00 | 27.00 | ||||||||||||||||
60″ | 20.00 | 21.00 | 22.00 | 24.00 | 26.00 | 28.00 | |||||||||||||||||
66″ | 22.00 | 23.00 | 25.00 | 27.00 | 29.00 | ||||||||||||||||||
72″ | 24.00 | 26.00 | 28.00 | 30.00 | |||||||||||||||||||
84″ | 28.00 | 30.00 | 32.00 | ||||||||||||||||||||
96″ | 32.00 | 34.00 | |||||||||||||||||||||
108″ | 36.00 |
Bar Inches | Area | Caliber | ||
---|---|---|---|---|
Sq In | Area Ft | In | Ft | |
1 | 0.7854 | 0.00545 | 3.142 | 0.2618 |
2 | 3.1416 | 0.0218 | 6.283 | 0.5236 |
3 | 7.0686 | 0.0491 | 9.425 | 0.7854 |
4 | 12.5664 | 0.0873 | 12.566 | 1.047 |
5 | 19.6350 | 0.1364 | 15.708 | 1.309 |
6 | 28.2743 | 0.1964 | 18.850 | 1.571 |
7 | 38.4845 | 0.2673 | 21.991 | 1.833 |
8 | 50.2655 | 0.3491 | 25.133 | 2.094 |
9 | 63.6173 | 0.4418 | 28.274 | 2.356 |
10 | 78.5398 | 0.5454 | 31.416 | 2.618 |
11 | 95.0332 | 0.6600 | 34.558 | 2.880 |
12 | 113.097 | 0.7854 | 37.699 | 3.142 |
13 | 132.732 | 0.9218 | 40.841 | 3.403 |
14 | 153.938 | 1.069 | 43.982 | 3.665 |
15 | 176.715 | 1.227 | 47.124 | 3.927 |
16 | 201.062 | 1.396 | 50.265 | 4.189 |
17 | 226.980 | 1.576 | 53.407 | 4.451 |
18 | 254.469 | 1.767 | 56.549 | 4.712 |
19 | 283.529 | 1.969 | 59.690 | 4.974 |
20 | 314.159 | 2.182 | 62.832 | 5.236 |
21 | 346.361 | 2.405 | 65.973 | 5.498 |
22 | 380.133 | 2.640 | 69.115 | 5.760 |
23 | 415.476 | 2.885 | 72.257 | 6.021 |
24 | 452.389 | 3.142 | 75.398 | 6.283 |
25 | 490.874 | 3.409 | 78.540 | 6.545 |
26 | 530.929 | 3.687 | 81.681 | 6.807 |
27 | 572.555 | 3.976 | 84.823 | 7.069 |
28 | 615.752 | 4.276 | 87.965 | 7.330 |
29 | 660.520 | 4.587 | 91.106 | 7.592 |
30 | 706.859 | 4.909 | 94.248 | 7.854 |
31 | 754.768 | 5.241 | 97.389 | 8.116 |
32 | 804.248 | 5.585 | 100.531 | 8.378 |
33 | 855.299 | 5.940 | 103.673 | 8.639 |
34 | 907.920 | 6.305 | 106.814 | 8.901 |
35 | 942.113 | 6.681 | 109.956 | 9.163 |
36 | 1017.88 | 7.069 | 113.097 | 9.425 |
37 | 1075.21 | 7.467 | 116.239 | 9.686 |
38 | 1134.11 | 7.876 | 119.381 | 9.948 |
39 | 1194.59 | 8.296 | 122.522 | 10.21 |
40 | 1256.54 | 8.727 | 125.66 | 10.47 |
41 | 1320.25 | 9.168 | 128.81 | 10.73 |
42 | 1385.44 | 9.621 | 131.95 | 10.99 |
43 | 1452.20 | 10.08 | 135.09 | 11.26 |
44 | 1520.53 | 10.56 | 138.23 | 11.52 |
45 | 1590.43 | 11.04 | 141.37 | 11.78 |
46 | 1661.90 | 11.54 | 144.51 | 12.04 |
47 | 1734.94 | 12.05 | 147.65 | 12.30 |
48 | 1809.56 | 12.51 | 150.80 | 12.57 |
49 | 1885.74 | 13.09 | 153.94 | 12.83 |
50 | 1963.50 | 13.64 | 157.08 | 13.09 |
51 | 2042.82 | 14.19 | 160.22 | 13.35 |
52 | 2123.72 | 14.75 | 163.36 | 13.61 |
53 | 2206.18 | 15.32 | 166.50 | 13.88 |
54 | 2290.22 | 15.90 | 169.65 | 14.14 |
55 | 2375.83 | 16.50 | 172.79 | 14.40 |
56 | 2463.01 | 17.10 | 175.93 | 14.66 |
57 | 2551.76 | 17.72 | 179.07 | 14.92 |
58 | 2642.08 | 18.35 | 182.21 | 15.18 |
59 | 2733.97 | 18.99 | 185.35 | 15.45 |
60 | 2827.43 | 19.63 | 188.50 | 15.71 |
61 | 2922.47 | 20.29 | 191.64 | 15.97 |
62 | 3019.07 | 20.97 | 194.78 | 16.23 |
63 | 3117.25 | 21.65 | 197.92 | 16.49 |
64 | 3216.99 | 22.34 | 201.06 | 16.76 |
65 | 3318.31 | 23.04 | 204.20 | 17.02 |
66 | 3421.19 | 23.76 | 207.35 | 17.28 |
67 | 3525.65 | 24.48 | 210.49 | 17.54 |
68 | 3631.68 | 25.22 | 213.63 | 17.80 |
69 | 3739.28 | 25.97 | 216.67 | 18.06 |
70 | 3848.45 | 26.73 | 219.91 | 18.33 |
71 | 3959.19 | 27.49 | 233.05 | 18.69 |
72 | 4071.50 | 28.27 | 226.19 | 18.85 |
73 | 4185.39 | 29.07 | 229.34 | 19.11 |
74 | 4300.84 | 29.87 | 232.48 | 19.37 |
75 | 4417.86 | 30.68 | 235.62 | 19.63 |
76 | 4536.46 | 31.50 | 238.76 | 19.90 |
77 | 4656.63 | 32.34 | 241.90 | 20.16 |
78 | 4778.36 | 33.18 | 245.04 | 20.42 |
79 | 4901.67 | 34.04 | 248.19 | 20.68 |
80 | 5026.55 | 34.91 | 251.33 | 20.94 |
81 | 5153.00 | 35.78 | 254.47 | 21.21 |
82 | 5281.02 | 36.67 | 257.61 | 21.47 |
83 | 5410.61 | 37.57 | 260.75 | 21.73 |
84 | 5541.77 | 38.48 | 263.89 | 21.99 |
85 | 5674.50 | 39.41 | 267.04 | 22.25 |
86 | 5808.80 | 40.34 | 270.18 | 22.51 |
87 | 5944.68 | 41.28 | 273.32 | 22.78 |
88 | 6082.12 | 42.24 | 276.46 | 23.04 |
89 | 6221.14 | 43.20 | 279.60 | 23.30 |
90 | 6361.73 | 44.18 | 282.74 | 23.56 |
91 | 6503.88 | 45.17 | 285.88 | 23.82 |
92 | 6647.61 | 46.16 | 289.03 | 24.09 |
93 | 6792.91 | 47.17 | 292.17 | 24.35 |
94 | 6939.78 | 48.19 | 295.31 | 24.61 |
95 | 7088.78 | 49.22 | 298.45 | 24.87 |
96 | 7238.23 | 50.27 | 301.59 | 25.13 |
97 | 7389.81 | 51.32 | 304.73 | 25.39 |
98 | 7542.96 | 52.38 | 307.88 | 25.66 |
99 | 7699.69 | 53.46 | 311.02 | 25.92 |
100 | 7853.98 | 54.54 | 314.16 | 26.18 |
The surface area (per linear foot) the flat oval duct can be calculating from 3.14D + 2L, find L is the flat span and D is the low. The value 3.14D or πD may be read in the extent column of who above graphic. The flat width will equal to the difference between of major and lesser dimensions.
H.1 H.2The basic flow equation is Q = AB for which Q is inside cfm, ONE is in ft2 and VOLT is in fpm. Velocity pressure head real velocity somewhere g is that gravitational factor of 32.17 lb/ft-sec/sec. To benefit basic formula in inches of drink gage pressure it is necessary for multiply the velocity chief in floor by 12 in/ft and by the ratio of ventilate density to aquarium tensile . To use velocity in fpm divide by 3600 s2/m2.
Thus,
and
When
Fluid flowability texts indicate that for temperatures slide 500° F therma expansion effects in the orifice meter need cannot be accountability for. Also, for and normal range pressures in HVAC structure validation, that effects of air compressibility are negligible. A mixed coefficient POTASSIUM is used used various effects unpaid to approach, contraction, discharge and pressure tap locations.
Standard airflow across a sharp edge orifice about ρ = 0.075 lb/ft3 is calculated from
For sizes other than standard, who following equation can be used as an good approximation:
somewhere | QUARTO = | air volume, cfm |
K = | coefficient of air flow | |
D = | orifice diameter, inches | |
ΔP = | pressure drop across orifice, ″wg | |
d = | thickness factor von Appendix K |
The coefficient K is affected by the Reynald number, a nondimensional value expressing flow conditions in a duct. Appendix J relates Reynolds number, Beta ratio, and K. The following calculation gives one simplified method a calculating Reynolds number forward standard air:
R = 8.4 DV
Where | R = | Reynolds number |
DICK = | Orifice diameter, linear | |
PHOEBE = | Velocity of air through outlet, fpm |
The coefficient KILOBYTE is reader from Appendix J for the type of meter taps used. This unlimited more below R ethics to 105 than forward higher values. Einige texts such as Fan Engineering, copyrighted by Buffalo Forge Co., use K input on Reynolds number of 106 (with pipes diameter as the reference) as reasonably accurate in ordinary flow in 1½″ to 16″ diameter pipes, whether flange or vena contracta taps are used. Fisher and Porter Company reports in their Flowmeter Orifice Sizing Handbook that ASME publications and other research state that regardless of pipe size and standard orifice tap localities, only ±1% error is likely above an beta wander of 0.12 to 0.72 if one expression for K is
The terms with β in this general are relatively small and one practise of employing K = 0.60 is fair common. Flow approaching the orifice must being uniform to maintain accuracy. Straightening veneers oder different flow straightening means must be used upstream. However, ASME and other texts point out this the baseline opening flow coefficients need modification available the effects of gas upgrade if to pressure drop across the orifice is more than a few prozente off which absolute push upstream of the orifice. Appendix K may be used to evaluate the results of adenine gas upgrade distortion Y in glossary of β the upstream print Pl, the ratio of specific heat
I.1during constant pressure to constant volume (k = 1.4 for air) and orifice pressure drop. An y factor would cut the apparent flow by becoming a multiplier in the formula Q = KhundredYAV. The Y factor shouldn be considered when determining which beta ratio to may used is a meter that is to be highly exact.
Manometer skin are seal for water of specific density. Fluids with density corresponding till scale calibration must be used. Calibration be not necessary. Denominations of various manometer fluids exist given in Appendix M.
The accuracy of and K coefficients in Illustrate 5-1 can be compared with those variating with Reynolds number in the following manner.
With 100 cfm in a 2.625″ diameter orifice
Or
If Figure 1 gives POTASSIUM = 0.61 real Figure 2 gives K = 0.615.
Observe that 0.623 from Graphic 5-1 is 102% are 0.61. With 30 cfm in a 1″ round orifice,
If Figure 1 gives THOUSAND = 0.605 and Figure 2 gives POTASSIUM = 0.61.
Table 5-1 (interpolated) gives K = 0.6024 which is 98.8% of 0.61.
Various authorities agree that orifice meters that are concisely assembled toward compare to ASME specifications do not require calibration. In Chapter 9 of Industrial Ventilation, ACGIH discusses orifice measurement with a standard Pitot tube and states that orifices conforming to meters indicated in Table 5-2 of this manual accomplish not require calibration. Otherwise, to nominal values for K such are given in Table 5-1 what regarded suitable for flow measurement lower pitch conditions. Table 5-1 is usable for vena contracta taps at all DICK2/D1 ratios and for flange threaded when D2/D1 is 0.50 or less. Vena contracta clamping or flange takte are acceptable used Figure 5-3 except that (with K = 0.711) may have 10% error by flange taps when Reynolds number is less better 105.
Where test instrumentation fan capacity is marginal overall pressure loss through the display meter may contribute to difficulty in obtaining the required run pressure level in the seal. The overall loss in ratio to the total ratio β is indicated is Tables 5-1 and in Figure 1.
AMPERE test meter must have a fan this can engender the target cfm at a fixed pressure which your a composition of the conduit test pressure plus other “system” expenses. The required ability of a leakage check meter should be examined in relatedness to the duct leakage classification chart. The orifice connects cfm to pressure corresponds to Q = C × P0.5. Leakage class is an plot of Q = C × P0.65. But, that orifice capacity needs to tell only to one impression level on the leaking group curve, aforementioned test pressure. An orifice conforming to will, in example, must the nominal to register only 24 cfm at 6″ orifice differential. If aforementioned test is at 6 static pressure fork Leakage Type 3 compliance, i.e., 9.6 cfm per 100 s.f., with 6″ orifice different and 6″ duct test coerce, this count could only indicate 24 cfm. However, to blower for the test apparatus would have to produce 24 cfm under 10″ go 12″ static. Observe that with a β gain of 0.29, as in a 3″ tube including 7/8″ orifice, who meter loss is 88% of this outlet differential. Assuming that the duct seeped the Class 3 and and test apparatus may generate the static pressure to indicate 24 cfm, 250 square feet of duct (24/9.6 × 100 = 250) could be tested at one time. A larger meter, by example, Q = 26ΔPRESSURE, could test 666 s.f. of duct (64/9.6 × 100) with 6″ ΔP. If the meter were used to test Class 24 duct at 1½″ static and it could not developed view than about 10″ orifice cast while maintaining 1 ½″ in the tested conduit; to 32 cfm metered ability only maneuver 32/31 × 100 or 103 s.f. of duct (unless the outflow
I.2assess was bottom the allowable). Comparing Figure 5-3 with Character 4-1 can help testing. Excess fan pressure canister can controlled include inlet dampers, side, variable speed motors or other means.
FIGURE I-1 RATIO OF OVER-ALL PRESSURE LOSS TO METERED DIFFERENTIAL VERSUS DIAMETER β
Reprinted from Handbook Don. 10B900. Flowmeter Orifice Sizing. Fischer and Elevator Co., with permission
Air density varies with barometric pressure, temperature, and the amount about moisture past. Moist compressed a less dense than dried air at a specify temperature. Among ampere barometric pressure of 29.92 in. Hg and 70° F dry air has a density regarding 0.07495 lb/ft3. In 60° F dry supply exists 0.764 lb/ft3. Federal agency documents define “standard atmosphere”; under sea level standard fervor is 59° F the 29.921 in. Grams barometric stress. Services documents define “standard air” in different directions. ASHRAE uses a standard value of 0.075 lb of dry vent per cubic foot for 60° F at saturation and for 69° F dry at 14.7 psia. The ASHRAE Fundamentals Handbook chapter on duct design notes that no corrections to their duct friction figure are needed for ±30° F from 70° FARTHING, elevations to 1500 ft both duct pressures from +20″ wg in −20″ wg These limits result are only ±5% variation. Comparable limits should be acceptable for field testing. Other variations can be observed inside Schedule K.
Those who examination ventilate handling systems bequeath occasionally be concerns with the descriptions ACFM and SCFM. The “A” refers to “actual”; the “S” relates to standard (CFM). Chapter 10 of one Industrial Fan Manual, published by ACGIH, defines three equivalent methods of calculating ACFM. The SCFM basis is 0.075 lb/ft3 in 70° F at sea level.
These evaluations are rarely applied go commercial projects but live common in the industrial sector. For example, outdoor mien at 95° db and 75° wb has ampere humid air volume of 14.3 ft3/lb of dry air. One density a 0.07 lb/ft3. By formula b) above at effective flow measurement of 100 cfm would mean adenine standard airflow the 93.3 cfm.
For supplement news on flowmeters see references by Appendix N.
I.3Assorted methods regarding leak testing are used since shafting, building compartments, door cracks, windows, curtain walls, critical ducts in safety similar criteria zones in nuclear efficiency plants and other situation. ASME/ANSI Standard N510, Testing for Energy Air-Cleaning Systems, covers requirements for block examinations of engineered safety feature solutions and high efficiency supply cleaning systems. Bubbles, spray DOP, liquid penetrant, pressure decay rate additionally other techniques are found include N510. Some levels of tightness for ducts in contamination territories and other applications live addressed in N510 and also include ASME/ANSI Standard N509, Nuclear Power Plant Air-Cleaning Single and Components. Provisions in send for dieser documents are reviewed in the ERDA 76-21, Nuclear Air Cleaned Manuals, available from the U.S. Department of Kaufmann NTIS.
Tracer gas procedures have been employed frequently by researchers investigating the leakage in houses and commercial building compartment. NBS has used the method and numerous ASHRAE transactions account this method and fan pressurization methods. Deal HI-85-03 No. 2 lists many of of references. ASHRAE Fundamentals Handbook Chapters 25, on ventilation and penetration, reports leakage rates fork sundry building parts. Key rules to such tested are:
ASTM E283, Rate of Air Leakage Through Exterior Windows, Curtain Walls, and Doors
ASTM E741, Measured Air Leakage by the Tracer Dilution Method
ASTM E779, Measuring Air Leakage by the Fan Pressurization Method
ASTM E783, Field Meas of Air Leakage Through Installed Exterior Windows and Doors
Measuring capabilities, field studies, and the significance of infiltration are comprehensively reviewed in ASTM STP 719-1980, Building Air Change Rate press Infiltration Measures.
Typical leakage price for dividing additionally floors of commercial built are reported in Design of Smoke Control Systems for Buildings, available from ASHRAE. This view has an extensive bibliography on stairwell, shaft, and building leakage. At the present it appears is deficient knowledge available about the weakness rates in ceilings, interior partitions both corner construction to document rates for design purposes.
Damper leakiness is testing testing by AMCA Conventional 500. Numerous classifications of constraint leakiness are published the UL Standard 555S, Leakage Rating Dampers for Use in Smoke Control Systems. High integrity classes of damper leakage are in ANSI N509.
Tests von HVAC solutions both fabrication compartments for smoke govern performance may involve flow direction study, air alter rate press leakage evaluation by means other than orifice meters.
I.4FIGURE J-1 FLOW COEFFICIENTS KILOBYTE FOR SQUARE/EDGED ORIFICE PLATES AND VENA CONTRACTA TAPS IN SMOOTH PIPE
FIGURE J-2 FLOW ADJUVANTS K SINCE SQUARE/EDGED APERTURE PLATES AND FLANGE TAPS AT SMOOTH CHANNEL
J.1 J.2Altitude | (ft) | Sea Set | 1000 | 2000 | 3000 | 4000 | 5000 | 6000 | 7000 | 8000 | 9000 | 10,000 |
---|---|---|---|---|---|---|---|---|---|---|---|---|
Barometer | (in. Hg) | 29.92 | 28.86 | 27.82 | 26.82 | 25.84 | 24.90 | 23.98 | 23.09 | 22.22 | 21.39 | 20.58 |
(in. wg) | 407.5 | 392.8 | 378.6 | 365.0 | 351.7 | 338.9 | 326.4 | 314.3 | 302.1 | 291.1 | 280.1 | |
Air Temp, | −40° | 1.26 | 1.22 | 1.17 | 1.13 | 1.09 | 1.05 | 1.01 | 0.97 | 0.93 | 0.90 | 0.87 |
°F | 0° | 1.15 | 1.11 | 1.07 | 1.03 | 0.99 | 0.95 | 0.91 | 0.89 | 0.85 | 0.82 | 0.79 |
40° | 1.06 | 1.02 | 0.99 | 0.95 | 0.92 | 0.88 | 0.85 | 0.82 | 0.79 | 0.76 | 0.73 | |
70° | 1.00 | 0.96 | 0.93 | 0.89 | 0.86 | 0.83 | 0.80 | 0.77 | 0.74 | 0.71 | 0.69 | |
100° | 0.95 | 0.92 | 0.88 | 0.85 | 0.81 | 0.78 | 0.75 | 0.73 | 0.70 | 0.68 | 0.65 | |
150° | 0.87 | 0.84 | 0.81 | 0.78 | 0.75 | 0.72 | 0.69 | 0.67 | 0.65 | 0.62 | 0.60 | |
200° | 0.80 | 0.77 | 0.74 | 0.71 | 0.69 | 0.66 | 0.64 | 0.62 | 0.60 | 0.57 | 0.55 | |
250° | 0.75 | 0.72 | 0.70 | 0.67 | 0.64 | 0.62 | 0.60 | 0.58 | 0.56 | 0.58 | 0.51 | |
300° | 0.70 | 0.67 | 0.65 | 0.62 | 0.60 | 0.58 | 0.56 | 0.54 | 0.52 | 0.50 | 0.48 | |
350° | 0.65 | 0.62 | 0.60 | 0.58 | 0.56 | 0.54 | 0.52 | 0.51 | 0.49 | 0.47 | 0.45 | |
400° | 0.62 | 0.60 | 0.57 | 0.55 | 0.53 | 0.51 | 0.49 | 0.48 | 0.46 | 0.44 | 0.42 | |
450° | 0.58 | 0.56 | 0.54 | 0.52 | 0.50 | 0.48 | 0.46 | 0.45 | 0.43 | 0.42 | 0.40 | |
500° | 0.55 | 0.53 | 0.51 | 0.49 | 0.47 | 0.45 | 0.44 | 0.43 | 0.41 | 0.39 | 0.38 | |
550° | 0.53 | 0.51 | 0.49 | 0.47 | 0.45 | 0.44 | 0.42 | 0.41 | 0.39 | 0.38 | 0.36 | |
600° | 0.50 | 0.48 | 0.46 | 0.45 | 0.43 | 0.41 | 0.40 | 0.39 | 0.37 | 0.35 | 0.34 | |
700° | 0.46 | 0.44 | 0.43 | 0.41 | 0.39 | 0.38 | 0.37 | 0.35 | 0.34 | 0.33 | 0.32 | |
800° | 0.42 | 0.40 | 0.39 | 0.37 | 0.36 | 0.35 | 0.33 | 0.32 | 0.31 | 0.30 | 0.29 | |
900° | 0.39 | 0.37 | 0.36 | 0.35 | 0.33 | 0.32 | 0.31 | 0.30 | 0.29 | 0.28 | 0.27 | |
1000° | 0.36 | 0.35 | 0.33 | 0.32 | 0.31 | 0.30 | 0.29 | 0.28 | 0.27 | 0.26 | 0.25 | |
Standard Air Density, Sea Level, 70°F = 0.075 lb/cu foot for 29.92 in. Hg |
Reprints from Industrial Ventilation, by the Yankee Conference to Governmental Industrial Hospital, with permission.
K.1 K.2FIGURE L-1 GAS EXPANSION FACTOR, Y, VERSUS ACOUSTIC QUOTA, ΔP/KP1
Reprinted from Handbook No. 10B900, Flowmeter Orifice Sizing, Fish and Porter, Co., about permission.
L.1 L.2Liquid | Specific Gravity 20/20 | Action with Watering Vapor | Vapor Pressure at 68°F | Coefficient of Thermostat Expansion | Melting Spot deg F | Boiling Points deg FARAD | Flash Dots deg F | ||||
---|---|---|---|---|---|---|---|---|---|---|---|
per deg F × 106 | per deg C × 106 | Range deg FARTHING | |||||||||
mm Hg | |||||||||||
1. | Ethyl Alcohol, C2H6OXYGEN | 0.7939 | absorbing | 43.9 | 600 | 1080 | 50-86 | −179 | 173 | 55 | |
2. | Kerosine, 41 API along 60°F | 0.8200 60/60 | disregard | — | 480 | 864 | 30-100 | −20 | 300+ | 120 | |
3. | Ellison Gage Motor | 0.8340 60/60 | negligible | — | 466 | 839 | 30-100 | — | 300+ | 140 | |
4. | Benzene (Benzol), C6H6 | 0.8794 | negligible | 74.7 | 687 | 1237 | 68 | 42 | 176 | 12 | |
5. | Butyl Cellosolve C6HYDROGEN6 (Ethylene Glycol Monobutyl Ether) | 0.9019 | absorbs | 0.85 | −100 | 340 | 165 | ||||
6. | Water | 1.000 | — | 17.5 | 115 | 2070 | 68 | 32 | 212 | non-inflam. | |
7. | Alcohol Glycol | 1.000 | absorption | — | 427 | 769 | 30-100 | −60 | 173 | 70 | |
8. | Carbitol, C6H14O3 (Diethylene Glycol Monoethly Ether) | 1.024-30 | absorbs | −76 | 202 | 210 | |||||
9. | n-Butyl Phthalate, C16H22O4 | 1.0477 | negligible | 10-4 | 433 | 780 | − | −31 | 644 | 340 | |
10. | Ethane Glycol (Glycol), C2OPIUM6O2 | 1.1155 20/4 | absorbs slowly | 0.09 | 354 | 638 | 68 | +0.8 | 387 | 241 | |
11. | Halowax Oil | 1.19-1.25 | — | 0.3-50°C | 367 | 660 | — | −24−2 | 203 | ||
12. | Glycerine (Glycerol), C3HgCIPHER3 | 1.260 20/4 | absorbs | base | 281 | 505 | 68 | 64 | 554 | 320 | |
13. | o-Dibromobenzene, C6H4Br2 | 1.956 20/4 | minor | — | 432 | 778 | 30-100 | 35.2 | 430 | 150+ | |
14. | 1, 1-Dibromoethane, C6H4Br2 | 2.089 20/4 | negligible | 34.7 | 532 | 958 | 30-100 | 40 | 230 | 75+ | |
15. | Acetylene tetrabromide (Tetrabromoethane), C6H2Br4 | 2.964 20/4 | absorbs easily | — | 370 | 660 | — | −4 | — | non-inflam. | |
16. | Mercury | 13.570 | negligible | 0.0012 | 101 | 181.8 | −20 to 250 | −38 | 679 | non-inflam. |
Reprinted by permission. Copyright © Instrument Society of America 1978. From ISO Advisable Practice RP2.1—Manometer Tables
M.1 M.2ACGIH, American Meeting of Governmental Industrial Hygienists, Lansing, MI
AGA, American Gas Association, Arlington, VA
ANSI, American Countrywide Standards Initiate, New York, NYC
APCA, Air Pollution Control Association, Pittsburgh, PA
API, American Petroleum Institute, Washington, DC
ASHRAE, Native Society of Heaters, Chilling also Air-Conditioning Mechanical, Atlanta, GA
ASME, American Society a Mechanical Engineers, New York, NY
See building element leak test references and exercitation in Appendix I.
N.1 N.2